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JP2008154576A - Method and apparatus for preparing rice flour - Google Patents

Method and apparatus for preparing rice flour Download PDF

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JP2008154576A
JP2008154576A JP2007212483A JP2007212483A JP2008154576A JP 2008154576 A JP2008154576 A JP 2008154576A JP 2007212483 A JP2007212483 A JP 2007212483A JP 2007212483 A JP2007212483 A JP 2007212483A JP 2008154576 A JP2008154576 A JP 2008154576A
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rice
steamed
water
drying
rice flour
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Yukinori Asano
幸紀 浅野
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ASANO SHOKUHIN KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method and apparatus for preparing rice flour, which are capable of providing rice flour having a wide potential application range in the future at a low cost by freely controlling the degree of gelatinization regardless of the kind of a rice raw material, and an apparatus therefor despite of a simple processing constitution and an easy process control. <P>SOLUTION: The preparation method of the rice flour includes a washing step 1B of washing rice, a water-absorption step 1C of soaking the washed rice in water at ordinary temperature for 20-120 min and subsequently draining the rice, a steaming step 1D of steaming the water-absorbed rice with saturated steam for a prescribed time to induce gelatinization of at least a portion of rice starch, a cooling step 1G of subjecting the steamed rice to rapid vacuum cooling until it reaches ordinary temperature, a maturation step 1H of maturing the gelatinized rice starch by leaving the steamed rice in a sterile condition for 24-48 hr, a drying step 1E of drying the matured rice by spraying superheated steam at 100-350°C under an ordinary pressure onto the matured rice flattened through a flattening step, and a powdering step 1F of grinding the dried rice into a powder. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、和洋菓子類、パン類、麺類などに使用できる、加工特性の優れた米粉の製造方法及びその装置に関する。  The present invention relates to a method and apparatus for producing rice flour having excellent processing characteristics that can be used in Japanese and Western confectionery, breads, noodles, and the like.

米を粉にする方式は、大別して、1.生米、すなわち米澱粉がベータ型の状態のままの米を粉砕して米粉を得る方式と、2.生米を熱処理して少なくとも米澱粉の一部をベータ型からアルファー型にした状態の米を粉砕して米粉を得る方式と、がある。この2方式のうち、1.の方式は、今まで団子やもちなどの和菓子に利用範囲が限定されていたが、最近微粉末にできるようになり、米粉パンを作るなどの試みがなされつつある。一方、2.の方式は、製造に手間がかかりコスト高になるため、古くから伝わる伝統的な和菓子に特化して使用されてきた。しかし、この方式で得られた米粉は、米澱粉をアルファー型にしているため、今後の技術開発も含めた展開を考えるとき、1.の方式によるベータ型の米粉よりも、その利用範囲が広がる可能性が高く、米の消費拡大につながる可能性が極めて高くなる。この米の消費について言えば、まず、日本人の食生活の多様化のため一人当たりの米の消費が減り続け、その上、小子高齢化により人口そのものが減るに至り、日本の米作中心の農業そのものの根幹を揺るがす事態に来て、米の消費拡大は待った無しの命題である。一方で、ウルグァイランドの関係から、外国産米(主としてインディカ種のタイ米)の輸入を義務付けられ、毎年10数万トン輸入され、この外国産米の消費も図らなければならない。したがって、米粉の利用範囲が今後広いと想定される2.のアルファー化米粉に注目する必要がある。  The methods for making rice flour can be broadly classified as follows: 1. A method of pulverizing raw rice, that is, rice in which the rice starch is in a beta-type state to obtain rice flour; There is a method in which raw rice is heat treated to pulverize rice in a state where at least a part of the rice starch is changed from a beta type to an alpha type to obtain rice flour. Of these two methods, This method has been limited to Japanese sweets such as dumplings and rice cakes, but recently it has become possible to make fine powder and attempts are being made to make rice flour bread. On the other hand, 2. This method has been used exclusively for traditional Japanese confectionery since ancient times because it takes time and cost to manufacture. However, since the rice flour obtained by this method uses rice starch in the alpha form, when considering development including future technological developments: Compared with the beta-type rice flour by this method, the range of use is more likely to expand, and the possibility of leading to increased consumption of rice becomes extremely high. Speaking of this rice consumption, first of all, the consumption of rice per person continues to decrease due to the diversification of Japanese diet, and furthermore, the population itself decreases due to the aging of the babies, Coming to a situation that shakes the foundations of agriculture itself, expanding rice consumption is a promising proposition. On the other hand, due to Uruguay's relations, it is obliged to import foreign rice (mainly Indica Thai rice), and 100,000 tons are imported every year, and this foreign rice must be consumed. Therefore, it is assumed that the range of utilization of rice flour will be wide in the future. It is necessary to pay attention to alpha rice flour.

このアルファー化米粉は、古来より、寒梅粉、道明寺粉、みじん粉、上南粉、乳児用粉などが有り、それらの製法は、粳米や糯米などの原料米を洗浄し、水に浸漬し水切り後、蒸すなどの熱処理を施して、米澱粉をベータ型からアルファー型に変え、その後搗いてもちにしそれを乾燥し、更に粉砕して粉にするものである。上記のような伝統的なアルファー化米粉の製造方法に対し、最新の工業的なアルファー化米粉の製造方法として、以下のようなものが知られている。  This alpha rice flour has been used since ancient times in the form of ume powder, Domyoji powder, vine flour, Kaminan flour, and infant flour.These methods are used to clean raw rice such as sticky rice and glutinous rice, soak it in water and drain it. After that, heat treatment such as steaming is performed to change the rice starch from the beta type to the alpha type, and then the rice starch is sprinkled and dried, and further pulverized into a powder. In contrast to the traditional method for producing pregelatinized rice flour as described above, the following are known as the latest industrial methods for producing pregelatinized rice flour.

特開2002−45130号公報  JP 2002-45130 A 特開2004−47号公報  JP 2004-47 A 特開2005−287365号公報  JP 2005-287365 A 特開2006−174756号公報  JP 2006-174756 A

特許文献1のアルファー化米粉の製造方法は、原料米をそのまま、ある一定条件の下で湿熱処理、すなわち、アルファー化処理し、その湿熱処理した原料米を乾燥して、さらに、乾燥原料米を粉砕して米粉を得るものである。そして、この湿熱処理は、オートクレーブで90℃以上120℃未満で50分間から90分間行うものである。  In the method for producing alpha-rice rice flour of Patent Document 1, raw rice is directly subjected to wet heat treatment under a certain condition, that is, alpha-treated, and the wet-heat treated raw rice is dried. It is pulverized to obtain rice flour. This wet heat treatment is performed in an autoclave at 90 ° C. or higher and lower than 120 ° C. for 50 minutes to 90 minutes.

特許文献2のアルファー化米粉の製造方法は、原料米を15℃〜30℃の水に15時間から20時間程度浸漬し吸水させた後、蒸気・マイクロ波または煮沸などにより加熱並びに滅菌処理し、さらに乾燥して、その乾燥原料米を粉砕して米粉を得るものである。その乾燥原料米を粉砕する際、研削式搗き精機により米粉を選択的に、例えば、原料米の表面部と内心部とに分け取りしたり、これらを粉体あるいは粒体に分け取りするものである。  The method for producing the pregelatinized rice flour of Patent Document 2 is that the raw rice is immersed in water at 15 ° C. to 30 ° C. for about 15 to 20 hours to absorb water, and then heated and sterilized by steam, microwave or boiling, It is further dried, and the dried raw rice is pulverized to obtain rice flour. When pulverizing the dried raw rice, the rice flour is selectively separated by a grinding-type milling machine, for example, divided into the surface portion and inner core portion of the raw rice, or divided into powder or granules. is there.

特許文献3のアルファー化米粉の製造方法は、原料米を洗浄し浸漬して水分値を30%〜35%に吸水させた後、粉砕して粉にし、この粉に温度を調節して熱風乾燥すると共に分級して希望する米粉を一の装置内で得るものである。そして、熱風乾燥する温度を米澱粉がアルファー化する温度にすれば、アルファー化した米粉が得られ、アルファー化する温度未満であれば、米澱粉がベータ型のままの米粉を得ることが出来るものである。  The manufacturing method of the pregelatinized rice flour of Patent Document 3 is that the raw rice is washed and soaked to absorb moisture to 30% to 35%, then pulverized into powder, and the temperature of the flour is adjusted and dried with hot air At the same time, it classifies and obtains the desired rice flour in one apparatus. And, if the temperature for hot air drying is set to a temperature at which the rice starch is alpha, the alpha starch is obtained, and if the temperature is below the alpha, the rice starch can be obtained in the beta form. It is.

特許文献4のアルファー化米粉の製造方法は、原料米ままあるいは洗浄し浸漬して吸水させた後、常圧下で1分から5分以内で原料米の品温を120℃から150℃に達するように高温の熱風空気で急速加熱して、原料米に簡易な膨化を起こさせ、この膨化原料米を粉砕して米粉を得るものである。  In the method for producing pre-alpha rice powder of Patent Document 4, the raw material rice is allowed to reach the temperature of 120 ° C. to 150 ° C. within 1 to 5 minutes under normal pressure after washing or dipping and absorbing water. Rapid heating with high-temperature hot-air air causes the raw rice to expand easily, and the expanded raw rice is pulverized to obtain rice flour.

特許文献1のアルファー化米粉の製造方法は、その原料米に対する湿熱処理を、明細書に記載されているオートクレーブにて行い、最終的に得られた米粉がX線回析装置にて測定した際、得られたX線回析相対強度がそれぞれの条件下で、相対ピーク強度が0.012〜0.023、0.030〜0.070、0.030〜0.060のうち2つ以上に該当するように、湿熱処理を構成したものであるため、湿熱処理の構成が複雑で工業的生産に適さない。また、湿熱処理を単にオートクレーブで90℃以上120℃未満で50分間から90分間行うものであるとした場合は、装置構成上高価になる。さらに湿熱処理を45℃以上60℃未満の温水で6時間から48時間かけて行うものであるとした場合では、温水の衛生管理を高度に行わないと、雑菌の温床となり実用性に乏しい。  The method for producing pregelatinized rice flour of Patent Document 1 is that when the raw rice is subjected to wet heat treatment in an autoclave described in the specification, and finally obtained rice flour is measured by an X-ray diffraction apparatus. The relative X-ray diffraction relative intensities obtained are at least two of 0.012-0.023, 0.030-0.070, 0.030-0.060 under the respective conditions. Since the heat treatment is configured as applicable, the structure of the heat treatment is complicated and is not suitable for industrial production. Further, if the wet heat treatment is simply performed at 90 ° C. or more and less than 120 ° C. for 50 minutes to 90 minutes by an autoclave, the apparatus configuration is expensive. Furthermore, in the case where the wet heat treatment is performed for 6 hours to 48 hours with warm water of 45 ° C. or more and less than 60 ° C., if the hygienic management of the warm water is not performed to a high degree, it becomes a hotbed of various bacteria and lacks practical utility.

特許文献2のアルファー化米粉の製造方法は、その原料米を15℃〜30℃の水に15時間から20時間程度浸漬し吸水させた後、米澱粉をアルファー化させるための加熱並びに滅菌処理をするから、明細書の記載のとおり、浸漬時に雑菌の温床とならないようにするため、1〜2回の水替えを行わなければならず、その水替作業が煩わしく、その上浸漬時間が長いから超大型の浸漬タンクが必要になるなどの不利がある。  In the method for producing pregelatinized rice flour of Patent Document 2, the raw rice is soaked in water at 15 ° C. to 30 ° C. for about 15 to 20 hours to absorb water, and then heated and sterilized to alphalize the rice starch. Therefore, as described in the specification, in order not to become a hotbed of various bacteria at the time of immersion, water must be changed once or twice, the water change work is troublesome, and the immersion time is long. There are disadvantages such as the need for a super large immersion tank.

特許文献3のアルファー化米粉の製造方法は、その原料米を浸漬して水分値を30%〜35%にした後、粉砕、乾燥及び分級を一の装置内で行い米粉を得るものであるが、水分値が13%〜15%程度の原料米を30%〜35%にする具体例が開示されていない。本発明者らの知見では、常温の水(20℃)であれば3時間以上、40℃の湯でも約30分かかり、いずれにしても、大型の浸漬タンクが必要になったり、その衛生管理が高度になったりする。  In the method for producing pregelatinized rice flour of Patent Document 3, the raw rice is soaked to have a moisture value of 30% to 35%, and then pulverized, dried and classified in one apparatus to obtain rice flour. No specific example is disclosed in which raw rice having a moisture value of about 13% to 15% is made 30% to 35%. According to the knowledge of the present inventors, if it is normal temperature water (20 ° C.), it takes 3 hours or more and 40 ° C. hot water takes about 30 minutes. Become advanced.

特許文献4のアルファー化米粉の製造方法は、原料米である玄米を常圧下で急速加熱して膨化させ粉化するものに有効であるとしても、精白米を原料にした場合、表面の米澱粉が糊化して、米同士の付着及び加熱釜に米が付着する現象があり、精白米には適用出来ない。すなわち、玄米には表皮、種皮及び果皮などの固い表層部分があり、この表層部分により米澱粉が包まれているから、上記の付着がないからである。  Even if the method for producing alpha-rice rice flour of Patent Document 4 is effective for brown rice, which is a raw material rice, that is rapidly heated under normal pressure to be expanded and pulverized, when polished rice is used as a raw material, the surface rice starch Is pasted, and there is a phenomenon in which rice adheres to each other and the rice adheres to the heating kettle, and cannot be applied to polished rice. That is, brown rice has hard surface layer portions such as the epidermis, seed coat and pericarp, and the rice starch is wrapped by this surface layer portion, so there is no such adhesion.

そこで、本発明の目的は、処理構成が単純であり、その処理工程の管理が容易であるのに、原料米の種類を問わずにアルファー化度を自由に調節して、その利用範囲が今後拡大すると期待できる米粉を、低コストで得ることが出来る米粉の製造方法及びその装置を提供することにある。  Therefore, the object of the present invention is that the processing configuration is simple and the management of the processing process is easy, but the alpha range can be freely adjusted regardless of the type of raw rice, and the range of use will be expanded in the future. An object of the present invention is to provide a rice flour production method and apparatus capable of obtaining rice flour that can be expected to expand at low cost.

本発明は、上記目的を達成するために提案されたものであって、下記の構成からなることを特徴とするものである。
すなわち、本発明によれば、米を洗浄する洗浄工程と、その洗浄後の米を常温の水に20分間〜120分間浸漬してから水切りする吸水工程と、その吸水後の米を飽和水蒸気で予め設定した時間蒸して、少なくとも米澱粉の一部をアルファー化する蒸し工程と、その蒸し米に100℃〜350℃の常圧過熱水蒸気を吹き付けて乾燥する乾燥工程と、その乾燥米を粉砕して粉にする粉化工程と、を含んでなることを特徴とする米粉の製造方法が提供される。
The present invention has been proposed in order to achieve the above object, and is characterized by having the following configuration.
That is, according to the present invention, a washing step for washing rice, a water absorption step for immersing the washed rice in normal temperature water for 20 to 120 minutes and then draining, and the rice after the water absorption with saturated steam Steaming for a preset time to alphalize at least a portion of the rice starch, drying step by spraying the steamed rice with normal pressure superheated steam at 100 ° C to 350 ° C, and crushing the dried rice There is provided a method for producing rice flour characterized by comprising a pulverizing step.

また、本発明によれば、前記蒸し工程と前記乾燥工程との間に、蒸し米を急速に真空冷却して常温にする冷却工程と、その常温の蒸し米を無菌状態にて24時間〜48時間放置しアルファー化した米澱粉を熟成させる熟成工程と、を付加させた米粉の製造方法が提供される。  In addition, according to the present invention, between the steaming step and the drying step, the steamed rice is rapidly vacuum-cooled to room temperature, and the steamed rice at room temperature is in a sterile state for 24 hours to 48 hours. There is provided a ripening step of aging rice starch that has been allowed to stand for a period of time, and a method for producing rice flour having added thereto.

また、本発明によれば、前記洗浄工程は、ネット上を所定量ずつ流通している米にエアー及び霧を吹き付け洗浄し且つ100℃〜350℃の常圧過熱水蒸気を吹き付けて殺菌してなる米粉の製造方法が提供される。  Further, according to the present invention, the cleaning step is performed by spraying air and mist on the rice flowing in a predetermined amount on the net and sterilizing by spraying normal pressure superheated steam at 100 ° C to 350 ° C. A method for producing rice flour is provided.

また、本発明によれば、前記洗浄工程は、ネット上を所定量ずつ流通している米にエアーを吹き付けると共に吸引して粗洗浄し、その粗洗浄後の米に霧を吹き付けると共に吸引して本洗浄して、その本洗浄後の米にエアーを吹き付けると共に吸引して仕上げ洗浄し、さらにその仕上げ洗浄後の米に100℃〜350℃の常圧過熱水蒸気を吹き付けて殺菌してなる米粉の製造方法が提供される。  Further, according to the present invention, the cleaning step is performed by blowing air and sucking and coarsely cleaning the rice flowing through the net by a predetermined amount, and spraying and sucking fog after the rough cleaning. The main washing is performed by spraying air on the washed rice and sucking it for finishing washing. Further, the finished washing rice is sprayed with normal pressure superheated steam at 100 ° C to 350 ° C to sterilize the rice flour. A manufacturing method is provided.

また、本発明によれば、前記蒸し工程と前記乾燥工程との間に、蒸し米を潰して板状にする平板化工程を付加させた米粉の製造方法が提供される。  Moreover, according to this invention, the manufacturing method of the rice flour which added the flattening process which crushes steamed rice and makes it plate shape between the said steaming process and the said drying process is provided.

また、本発明によれば、前記熟成工程と前記乾燥工程との間に、熟成米を潰して板状にする平板化工程を付加させた米粉の製造方法が提供される。  Moreover, according to this invention, the manufacturing method of the rice flour which added the flattening process which crushed aged rice into a plate shape between the said ripening process and the said drying process is provided.

また、本発明によれば、米貯留タンクから所定量ずつネット上に受け入れた米にエアー及び霧を吹き付け洗浄し且つ100℃〜350℃の常圧過熱水蒸気を吹き付けて殺菌する洗浄殺菌部と、その洗浄殺菌後の米を30℃〜48℃の湯に20秒間〜10分間さらしてから水切りをする吸水部と、吸水水切り後の米を一定量貯留するタンクの底板及び側板の多数の孔より0.25kg/cm〜1.5kg/cmの飽和蒸気を予め設定した時間吹き込んで蒸し、かつ内部に米を一定量排出する定量フィーダーを有してなる蒸し機と、その蒸し米に100℃〜350℃の常圧過熱水蒸気を吹き付けて乾燥する乾燥部と、その乾燥米を粉砕して粉にする粉化部と、を含んでなることを特徴とする米粉の製造装置が提供される。In addition, according to the present invention, a cleaning and sterilization unit for cleaning by spraying air and mist on the rice received on the net by a predetermined amount from the rice storage tank and sterilizing by spraying normal pressure superheated steam at 100 ° C to 350 ° C, The water-absorbing part that drains water after exposing the washed and sterilized rice to hot water of 30 ° C. to 48 ° C. for 20 seconds to 10 minutes, and a plurality of holes in the bottom plate and side plate of the tank that stores a certain amount of rice after draining the water. and 0.25kg / cm 2 ~1.5kg / cm steamed 2 of the saturated steam blown preset time, and the internal comprising a metering feeder for a predetermined amount of discharging the rice steamed machine 100 to the steamed rice There is provided a rice flour production apparatus comprising: a drying section that sprays and dries atmospheric pressure superheated steam at ℃ to 350 ° C; and a pulverization section that pulverizes the dried rice into powder. .

また、本発明によれば、前記蒸し機と前記乾燥部との間に、蒸し米を受け入れ予備ほぐしを行うと共にその所定量を計量する計量機と、計量された蒸し米を容器内に入れ閉じて690mmHg以上の真空状態を10秒間〜30秒間保持するようにして常温にしたあと前記容器内から蒸し米を取り出す真空冷却機と、アルファー化した米澱粉を熟成させたあと蒸し米を本ほぐしを行って単粒化した状態とする熟成ほぐし部と、を付加させた米粉の製造装置が提供される。  Further, according to the present invention, between the steamer and the drying unit, the steamed rice is received and preliminarily loosened and a predetermined amount is weighed, and the weighed steamed rice is put in a container and closed. A vacuum cooler that takes out steamed rice from the vessel after maintaining the vacuum state at 690 mmHg or more for 10 to 30 seconds and then ripening the steamed rice after aging the pregelatinized rice starch. An apparatus for producing rice flour to which a ripening loosening portion that is made into a single grain is added is provided.

また、本発明によれば、前記蒸し機と前記乾燥部との間に、無端ベルトとロールとの間に蒸し米を通すことで潰して板状にする平板加工機を付加させた米粉の製造装置が提供される。  Moreover, according to this invention, the manufacture of the rice flour which added the flat plate processing machine made into a plate shape by crushing steamed rice between an endless belt and a roll between the said steamer and the said drying part. An apparatus is provided.

また、本発明によれば、前記熟成ほぐし部と前記乾燥部との間に、無端ベルトとロールとの間に熟成米を通すことで潰して板状にする平板加工機を付加させた米粉の製造装置が提供される。  Further, according to the present invention, between the aging loosening portion and the drying portion, the rice flour added with a flat plate processing machine that crushes the aging rice by passing the aging rice between an endless belt and a roll. A manufacturing apparatus is provided.

本発明の米粉の製造方法によれば、洗浄した後の米を、常温の水に20分間〜120分間浸漬して吸水させてから水切りし、飽和水蒸気で米澱粉が設定したアルファー化度になるまで蒸して、その蒸し米に100℃〜350℃の常圧過熱水蒸気を吹き付けて乾燥し、さらに粉砕して米粉を得る。したがって、すでに蒸してある蒸し米を常圧過熱水蒸気により乾燥して粉にするだけなので、処理構成が単純であり、その処理工程の管理も容易なのに、原料米の種類を問わず設定したアルファー化度の米粉を得ることが出来る。加えて、飽和水蒸気の蒸し時間を調整することで、米澱粉のアルファー化度を容易に変えることが出来、また、常圧過熱水蒸気はほぼ無酸素状態であるから、ビタミンや酵素などに対して酸素による影響がほとんど無く、殺菌効果も高く、このような米粉は今後その利用範囲が拡大すると期待できる。  According to the method for producing rice flour of the present invention, the washed rice is soaked in water at room temperature for 20 to 120 minutes to absorb water, drained, and the degree of alpha starchation set by saturated steam becomes rice starch. Steamed to 100 ° C to 350 ° C under normal pressure superheated steam, dried and further pulverized to obtain rice flour. Therefore, since steamed rice that has already been steamed is simply dried to form powder with atmospheric superheated steam, the processing configuration is simple and the processing process is easy to manage. You can get the right rice flour. In addition, by adjusting the steaming time of saturated steam, the alpha degree of rice starch can be easily changed, and atmospheric superheated steam is almost oxygen-free, so it can be used for vitamins and enzymes. There is almost no influence by oxygen, and the bactericidal effect is high, and it can be expected that such rice flour will be used in the future.

また、本発明の米粉の製造方法によれば、飽和水蒸気による蒸し米を、乾燥する前に急速真空冷却して常温にし、その常温蒸し米を無菌状態にて24時間〜48時間放置してアルファー化米澱粉を熟成させてから、その熟成米に対し常圧過熱水蒸気を吹き付けて乾燥し、さらに粉砕して米粉を得る。したがって、上記効果に加えて、米澱粉のアルファー化状態を均質に固定でき、米粉にした後の利用を品質面で支えることができる。  In addition, according to the method for producing rice flour of the present invention, steamed rice with saturated steam is rapidly cooled to room temperature before drying, and the room temperature steamed rice is allowed to stand for 24 to 48 hours in an aseptic condition. After the matured rice starch is ripened, the steamed rice is dried by spraying normal pressure superheated steam and further pulverized to obtain rice flour. Therefore, in addition to the above effects, the pregelatinized state of the rice starch can be fixed uniformly, and the use after making the rice flour can be supported in terms of quality.

また、本発明の米粉の製造方法によれば、その洗浄工程がネット上を所定量ずつ流通している米にエアー及び霧を吹き付け洗浄し、さらに常圧過熱水蒸気を吹き付けて、濡らさずしかも品温も上昇して殺菌する。したがって、上記効果に加えて、水をほとんど使用しないで米をスムーズに洗浄殺菌出来るから、洗米廃水もほとんど生じず、しかも、25℃以上の水に米を浸漬しても菌の繁殖がなく吸水時間の短縮も可能となり、廃水処理も含めた構成の単純化、小型化及び小スペース化を図れる。  Further, according to the method for producing rice flour of the present invention, the washing process is carried out by spraying air and mist on the rice that is circulated in a predetermined amount on the net, and further sprayed with atmospheric superheated steam to prevent the product from getting wet. The temperature rises and sterilizes. Therefore, in addition to the above effects, the rice can be washed and sterilized smoothly with little use of water, so there is almost no waste water from washing the rice, and even when the rice is immersed in water at 25 ° C or higher, there is no growth of bacteria and water absorption. The time can be shortened, and the configuration including wastewater treatment can be simplified, downsized, and reduced in space.

また、本発明の米粉の製造方法によれば、米にエアーを吹き付けると共に吸引して粗洗浄した後、米に霧を吹き付け洗浄し、その後再び米にエアーを吹き付け仕上げ洗浄を行い、その後、洗米に常圧過熱水蒸気を吹き付けて殺菌をする。したがって、上記効果に加えて、米の洗浄殺菌が完全となる。  Further, according to the method for producing rice flour of the present invention, after air is blown and sucked and coarsely washed, the rice is sprayed with mist and then washed again by blowing air onto the rice and then washed with rice. Sterilize by spraying normal pressure superheated steam. Therefore, in addition to the above effects, the rice is completely cleaned and sterilized.

また、本発明の米粉の製造方法によれば、飽和水蒸気による蒸し米を、乾燥する前に潰し板状にしてから、常圧過熱水蒸気を吹き付けて乾燥し、さらに粉砕して米粉を得る。したがって、上記効果に加えて、粒状の蒸し米を板状にした分乾燥時間を短縮できる。  Moreover, according to the method for producing rice flour of the present invention, steamed rice with saturated steam is made into a crushed plate before drying, then sprayed with atmospheric superheated steam, dried, and further pulverized to obtain rice flour. Therefore, in addition to the above effects, the drying time can be shortened by the amount of granular steamed rice made into a plate shape.

また、本発明の米粉の製造方法によれば、熟成米を乾燥する前に潰し板状にしてから、常圧過熱水蒸気を吹き付けて乾燥し、さらに粉砕して米粉を得る。したがって、上記効果に加えて、粒状の熟成米を板状にした分乾燥時間を短縮できる。  In addition, according to the method for producing rice flour of the present invention, ripened rice is crushed before drying, then dried by spraying atmospheric superheated steam, and further pulverized to obtain rice flour. Therefore, in addition to the above effects, the drying time can be shortened by the amount of granular aged rice made into a plate shape.

また、本発明の米粉の製造装置によれば、上記発明の米粉の製造方法をより効率よく実施でき、効率よくアルファー化した米粉を得ることが出来るから、その分従来のものよりメリットがある。  Moreover, according to the rice flour production apparatus of the present invention, the rice flour production method of the present invention can be more efficiently carried out, and an efficiently pregelatinized rice flour can be obtained.

また、本発明の米粉の製造装置によれば、蒸し機から出た蒸し米を計量機により予備ほぐし及び計量してから、真空冷却機に投入し常温にして、さらに熟成ほぐし部によりアルファー化米澱粉を熟成させて、その熟成米に本ほぐしを施して単粒化してから、乾燥部に送る。したがって、上記効果に加えて、米澱粉のアルファー化状態を均質にし、且つ米粉の利用を品質面で支えることを、装置的に可能とした。  According to the rice flour production apparatus of the present invention, the steamed rice from the steamer is preliminarily loosened and weighed with a weighing machine, and then put into a vacuum cooler to bring it to room temperature. The starch is aged, and the aged rice is subjected to regular unraveling to make a single grain, which is then sent to the drying section. Therefore, in addition to the above effects, it is possible to make it possible to homogenize the pregelatinized state of rice starch and support the use of rice flour in terms of quality.

また、本発明の米粉の製造装置によれば、蒸し機から出た蒸し米を、平板加工機の無端ベルトとロールとの間に通して、潰し板状にしてから乾燥部にて常圧渦熱水蒸気を吹き付けて乾燥する。したがって、上記効果に加えて、蒸し米の乾燥時間の短縮を装置的に可能とした。  Further, according to the rice flour producing apparatus of the present invention, the steamed rice from the steamer is passed between an endless belt and a roll of a flat plate processing machine to form a crushed plate, and then a normal pressure vortex in the drying section. Spray with hot steam to dry. Therefore, in addition to the above effects, the drying time of the steamed rice can be shortened as a device.

また、本発明の米粉の製造装置によれば、熟成ほぐし部から出た熟成米を、平板加工機の無端ベルトとロールとの間に通して、潰し板状にしてから乾燥部にて常圧過熱水蒸気を吹き付けて乾燥する。したがって、上記効果に加えて、熟成米の乾燥時間の短縮を装置的に可能とした。  Further, according to the rice flour production apparatus of the present invention, the aged rice from the aging unraveling part is passed between an endless belt and a roll of a flat plate processing machine to form a crushed plate and then normal pressure in the drying part. Spray with superheated steam to dry. Therefore, in addition to the above effects, the drying time of the ripened rice can be shortened as a device.

以下に、図面を参照して本発明を実施するための最良の形態を説明する。
図1は本発明の米粉の製造方法を示すフロシート図である。図面において、米粉の製造方法1Aは、米を洗浄する洗浄工程1Bと、その洗浄後の米を常温の水に20分間〜120分間浸漬してから水切りする吸水工程1Cと、その吸水後の米を飽和水蒸気で予め設定した時間蒸して少なくとも米澱粉の一部をアルファー化する蒸し工程1Dと、その蒸し米に100℃〜350℃の常圧過熱水蒸気を吹き付けて乾燥する乾燥工程1Eと、その乾燥米を粉砕して粉にする粉化工程1Fと、を含んでなるものであり、また、上記した蒸し工程1Dと乾燥工程1Eとの間に、蒸し米を急速に真空冷却して常温にする冷却工程1Gと、その常温の蒸し米を無菌状態で24時間〜48時間放置しアルファー化した米澱粉を熟成させる熟成工程1Hと、を付加させても良い。
The best mode for carrying out the present invention will be described below with reference to the drawings.
FIG. 1 is a flow sheet diagram showing the method for producing rice flour of the present invention. In the drawings, rice flour production method 1A includes a washing step 1B for washing rice, a water absorption step 1C for immersing the washed rice in normal temperature water for 20 to 120 minutes and then draining, and the rice after the water absorption. Steamed with saturated steam for a preset period of time to steamize at least a portion of the rice starch, drying process 1E for spraying the steamed rice with normal pressure superheated steam at 100 ° C to 350 ° C and drying, A pulverizing step 1F for pulverizing the dried rice, and between the steaming step 1D and the drying step 1E, the steamed rice is rapidly cooled to room temperature. A cooling step 1G to be performed and a maturing step 1H in which the steamed rice at room temperature is allowed to stand for 24 to 48 hours in an aseptic state to age the rice starch that has been pregelatinized may be added.

前記洗浄工程1Bは、従来公知の洗米機に単に米と水とを供給して洗浄しても良いし、後述のネット3上に所定量ずつ流通している米にエアー及び霧を吹き付け洗浄し、さらに100℃〜350℃の常圧過熱水蒸気を吹き付けて殺菌しても良い。この洗浄方法では、洗米廃水がほとんど生じず、しかも、25℃以上の水に米を浸漬しても菌の繁殖がなく、吸水時間の短縮も可能で且つ衛生管理が容易となる。また、この洗浄工程1Bは、ネット3上を所定量ずつ流通している米にエアーを吹き付けると共に吸引して粗洗浄し、その粗洗浄後の米に霧を吹き付けると共に吸引して本洗浄して、その本洗浄後の米にエアーを吹き付けると共に吸引して仕上げ洗浄し、さらにその仕上げ洗浄後の米に100℃〜350℃の常圧過熱水蒸気を吹き付けて殺菌しても良い。この洗浄方法では、エアーや霧を吹き付けるだけでなく、吸引するから米をより確実且つ充分に洗浄することができる。  The washing step 1B may be performed by simply supplying rice and water to a conventionally known rice washer, or by washing with air and mist sprayed on a predetermined amount of rice on the net 3 described later. Further, it may be sterilized by spraying normal pressure superheated steam at 100 ° C. to 350 ° C. In this washing method, waste water for washing the rice is hardly generated, and even if the rice is immersed in water at 25 ° C. or higher, there is no growth of bacteria, the water absorption time can be shortened, and hygiene management is facilitated. In addition, the cleaning process 1B blows air to the rice flowing through the net 3 by a predetermined amount and sucks and roughly cleans the rice. The rice after the main cleaning may be blown with air and sucked for finishing cleaning, and then the rice after the final cleaning may be sterilized by spraying normal pressure superheated steam at 100 ° C. to 350 ° C. This cleaning method not only blows air and mist, but also sucks, so that the rice can be more reliably and sufficiently cleaned.

前記吸水工程1Cは、米を常温の水にて20分間〜120分間浸漬し吸水させてから水切りしている。夏場の水温が高いときは下限値の20分間浸漬で良く、冬場の水温が低いときは上限値の120分間浸漬となる。20℃の水温であれば、30分間浸漬させれば充分吸水させることができる。また、後述するように、洗浄工程1Bにて米に常圧過熱水蒸気を吹き付け殺菌し品温上昇している場合は、30℃〜48℃の湯に20秒間〜10分間晒せば充分吸水するから、それから水切りをすれば良い。  In the water absorption step 1C, the rice is immersed in water at room temperature for 20 minutes to 120 minutes to absorb water and then drained. When the water temperature in summer is high, the lower limit value may be immersed for 20 minutes, and when the water temperature in winter is low, the upper limit value is immersed for 120 minutes. If it is 20 degreeC water temperature, it can be made to absorb water enough if it is immersed for 30 minutes. In addition, as will be described later, when the product temperature rises by spraying normal pressure superheated steam on the rice in the washing step 1B, water is sufficiently absorbed if exposed to hot water of 30 ° C. to 48 ° C. for 20 seconds to 10 minutes. Then drain it.

前記蒸し工程1Dは、米の蒸し時間を、例えば、1分間〜15分間の範囲で調整することで、米澱粉のアルファー化度を0%に近い値から100%に近い値まで自在に調整できる。したがって、米粉の使用目的に合わせたアルファー化度になるように蒸し時間を調整する。  The steaming step 1D can freely adjust the degree of alpha of rice starch from a value close to 0% to a value close to 100% by adjusting the steaming time of the rice within a range of, for example, 1 minute to 15 minutes. . Therefore, the steaming time is adjusted so as to achieve a degree of alpha conversion that matches the intended purpose of the rice flour.

前記乾燥工程1Eは、米の乾燥時間及び常圧過熱水蒸気の温度を調整することで、米の水分を自在に設定できる。したがって、米粉の使用目的に合わせた乾燥後水分、例えば、3重量%〜10重量%の範囲になるように、乾燥時間及び常圧過熱水蒸気の温度を調整する。ここでは、常圧過熱水蒸気を使用して乾燥させるから、熱含量が高いため乾燥が早く出来、無酸素状態であるから米に含有するビタミンや酵素などに対し、酸素による影響がほとんど無く、また、常圧過熱水蒸気の温度が120℃以上であれば殺菌効果も高く無菌状態となる。  In the drying step 1E, the moisture of the rice can be freely set by adjusting the drying time of the rice and the temperature of the atmospheric superheated steam. Therefore, the drying time and the temperature of the atmospheric superheated steam are adjusted so that the moisture after drying suitable for the purpose of use of the rice flour, for example, in the range of 3 wt% to 10 wt%. Here, drying is performed using normal-pressure superheated steam, so it can be dried quickly because of its high heat content, and since it is oxygen-free, there is almost no influence of oxygen on vitamins and enzymes contained in rice. If the temperature of the normal pressure superheated steam is 120 ° C. or higher, the sterilization effect is high and the sterilized state is obtained.

前記粉化工程1Fは、単に乾燥米を粉砕して粉にできれば良く、その方式、粉径に限定がない。米粉の使用目的に合わせて粉砕方式や粉径を設定する。  The said pulverization process 1F should just pulverize dried rice and can be made into a powder, and there is no limitation in the system and a powder diameter. The pulverization method and powder size are set according to the intended use of rice flour.

前記蒸し工程1Dと乾燥工程1Eとの間に付加する冷却工程1Gは、蒸し米を急速に真空冷却して常温にするものであり、さらに、熟成工程1Hは、アルファー化した米澱粉を熟成させるものである。これら2工程は、アルファー化した米澱粉を均質にし、米粉の品質向上に資するものである。なお、米粉の原料米は、粳米や糯米、新米や古米、玄米や精白米、ジャポニカ種やインディカ種など、特に限定がない。  The cooling step 1G added between the steaming step 1D and the drying step 1E is to rapidly cool the steamed rice to room temperature, and the ripening step 1H ripens the pregelatinized rice starch. Is. These two steps homogenize the pregelatinized rice starch and contribute to improving the quality of the rice flour. In addition, the raw material rice of rice flour is not particularly limited, such as glutinous rice and glutinous rice, new rice and old rice, brown rice and polished rice, japonica varieties and indica varieties.

次に、上記した米粉の製造方法を具体的に実施する米粉の製造装置について説明する。
図2は本発明の米粉の製造方法を具体化した製造装置のフロシート図、図3は本発明の米粉の製造装置における洗浄殺菌部のフロシート図、図4は本発明の米粉の製造装置における洗浄部の組立状態を示す斜視図、図5は本発明の米粉の製造装置における蒸し機の一部を切欠した斜視図である。図面において、米粉の製造装置1は、米貯留タンク2から所定量ずつネット3(図3に示す)上に受け入れた米にエアー及び霧を吹き付け洗浄し且つ100℃〜350℃の常圧過熱水蒸気を吹き付けて殺菌する洗浄殺菌部4と、その洗浄殺菌後の米を30℃〜48℃の湯に20秒間〜10分間さらしてから水切りをする吸水部5と、吸水水切り後の米を一定量貯留するタンク6の底板6a及び側板6bの多数の孔6c(図5に示す)より0.25kg/cm〜1.5kg/cmの飽和水蒸気を吹き込んで蒸しかつ内部に米を一定量排出する定量フィーダー7を有してなる蒸し機8と、その蒸し米を受け入れ予備ほぐしを行うと共にその所定量を計量する計量機9と、計量された蒸し米を複数の容器10内に順次入れ閉じて690mmHg以上の真空状態を10秒間〜30秒間保持するようにして常温にしたあと容器10内から蒸し米を取り出す真空冷却機11と、アルファー化した米澱粉を熟成させたあと蒸し米を本ほぐしを行って単粒化した状態とする熟成ほぐし部12と、その熟成後の蒸し米に100℃〜350℃の常圧過熱水蒸気を吹き付けて乾燥する乾燥部13と、その乾燥米を粉砕して粉にする粉化部14と、を含んでなるものである。
Next, a rice flour production apparatus that specifically implements the above-described method for producing rice flour will be described.
2 is a flow sheet diagram of a production apparatus embodying the rice flour production method of the present invention, FIG. 3 is a flow sheet diagram of a cleaning and sterilizing section in the rice flour production apparatus of the present invention, and FIG. 4 is a cleaning process in the rice flour production apparatus of the present invention. The perspective view which shows the assembly state of a part, FIG. 5 is the perspective view which notched some steamers in the rice flour manufacturing apparatus of this invention. In the drawing, a rice flour production apparatus 1 is a normal pressure superheated steam at 100 ° C. to 350 ° C. which is washed by blowing air and mist onto rice received on a net 3 (shown in FIG. 3) by a predetermined amount from a rice storage tank 2. The sterilization part 4 for sterilizing by spraying, the water absorbing part 5 for draining the washed and sterilized rice in hot water of 30 ° C. to 48 ° C. for 20 seconds to 10 minutes, and a fixed amount of rice after draining the water constant emissions many holes 6c by blowing saturated steam of 0.25kg / cm 2 ~1.5kg / cm 2 from (shown in FIG. 5) steamed and rice inside the bottom plate 6a and the side plate 6b of the tank 6 for storing A steaming machine 8 having a fixed quantity feeder 7, a weighing machine 9 for receiving the steamed rice and preliminarily loosening it, and weighing a predetermined amount thereof; 690mmH The above vacuum state is maintained for 10 seconds to 30 seconds, brought to room temperature, and then the vacuum cooler 11 for taking out the steamed rice from the container 10 and maturing the steamed rice after aging the alpha starch. Aged unraveling portion 12 that is made into a single grain state, drying portion 13 that is dried by spraying normal-temperature superheated steam at 100 ° C. to 350 ° C. to the steamed rice after aging, and pulverizing the dried rice into powder The powdering part 14 to be comprised.

前記米貯留タンク2は、その下部にロータリーバルブ15を設け、その下に搬送装置16を設けてあり、バルブ17を開くことで、前記洗浄殺菌部4における後述する米定量供給機30の受入タンク31に米を供給する。  The rice storage tank 2 is provided with a rotary valve 15 at a lower portion thereof, and a conveying device 16 is provided therebelow. By opening the valve 17, a receiving tank for a rice fixed-quantity feeder 30 to be described later in the cleaning and sterilization unit 4 is provided. Supply rice to 31.

前記洗浄殺菌部4は、洗浄部4Aと殺菌部4Bとに分かれ、洗浄部4Aは、図3、4に示すように、幅広のトヨ20にフタ21を取り付け、トヨ20の底板22に孔22aを開け、その孔22aに前記ネット3を張り、さらに、ネット3を境として底板22の外側にコーン状フード23を取り付け、トヨ20の側板24にエアー吹出管25、霧吹出管26及びエアー吹出管27を貫通させるための切欠部24a、24b、24cを設けている。トヨ20とフタ21とで囲う空間で加圧室28を形成し、トヨ20に張ったネット3とコーン状フード23とで囲う空間で減圧室29を形成する。ネット3はステンレスネットが採用され、そのメッシュは米粒が通過しない程度であれば良く、したがって、多孔板のようなものでも良い。  The cleaning and sterilizing unit 4 is divided into a cleaning unit 4A and a sterilizing unit 4B. As shown in FIGS. 3 and 4, the cleaning unit 4A has a lid 21 attached to a wide toyo 20 and a hole 22a in a bottom plate 22 of the toyo 20. , The net 3 is stretched in the hole 22a, a cone-shaped hood 23 is attached to the outside of the bottom plate 22 with the net 3 as a boundary, and the air blowing pipe 25, the mist blowing pipe 26 and the air blowing are attached to the side plate 24 of the toyo 20 Notches 24a, 24b and 24c for penetrating the tube 27 are provided. A pressurizing chamber 28 is formed in a space surrounded by the toyo 20 and the lid 21, and a decompression chamber 29 is formed in a space surrounded by the net 3 stretched on the toyo 20 and the cone-shaped hood 23. The net 3 is made of a stainless steel net, and the mesh may be of a size that does not allow rice grains to pass therethrough, and therefore may be a perforated plate.

前記洗浄部4Aに米を定量的に供給する米定量供給機30が設けられ、この米定量供給機30は、受入タンク31の下部に所定の傾斜を有する通路32に、振動機33を取り付けてなり、受入タンク31下部から通路32に入った米Rを、振動機33により通路32を振動させて、所定量の米を洗浄部4Aに供給する。なお、米の供給量の調整は振動機33の振動強度の変化により行う。  A rice fixed amount supply machine 30 for quantitatively supplying rice to the washing unit 4A is provided, and this rice fixed amount supply machine 30 has a vibrator 33 attached to a passage 32 having a predetermined inclination at a lower portion of the receiving tank 31. The rice R that has entered the passage 32 from the lower part of the receiving tank 31 is vibrated in the passage 32 by the vibrator 33 to supply a predetermined amount of rice to the cleaning unit 4A. The supply amount of rice is adjusted by changing the vibration intensity of the vibrator 33.

そして、エアー吹出管25、27は、ブロアー34に接続し、霧吹出管26は霧発生用ポンプ35に接続している。これらエアー吹出管25、27には無数の小孔が開けられ、無数の小孔からエアーが吹き出され、霧吹出管26には噴霧ノズル36が取り付けられ、霧が吹き出されるようになっている。また、減圧室29には真空ポンプ37が接続され、これら減圧室29と真空ポンプ37との間に米付着物除去タンク38が設置されている。この米付着物除去タンク38の下端にはロータリーバルブ39が取り付けられ、このロータリーバルブ39の下方に米付着物40を受けるためのトレ−41を置いている。したがって、除去された米付着物40は、真空ポンプ37を通過して外部に排出されることがなく、トレー41に回収される。  The air blowing pipes 25 and 27 are connected to the blower 34, and the mist blowing pipe 26 is connected to the mist generating pump 35. These air blowing pipes 25 and 27 have innumerable small holes, air is blown out from the innumerable small holes, and a spray nozzle 36 is attached to the mist blowing pipe 26 so that the mist is blown out. . A vacuum pump 37 is connected to the decompression chamber 29, and a rice deposit removal tank 38 is installed between the decompression chamber 29 and the vacuum pump 37. A rotary valve 39 is attached to the lower end of the rice deposit removal tank 38, and a tray 41 for receiving the rice deposit 40 is placed below the rotary valve 39. Therefore, the removed rice deposit 40 is collected in the tray 41 without passing through the vacuum pump 37 and being discharged to the outside.

前記殺菌部4Bは、過熱蒸気室42とこの中を走行する蒸気室コンベアー43とからなり、この過熱蒸気室42は、ボイラー44に常圧過熱水蒸気発生装置45を経由して接続している。この常圧過熱水蒸気発生装置45は、常圧過熱水蒸気を発生するものであり、この常圧過熱水蒸気は、通常のボイラー、例えば、ボイラー44から出た飽和水蒸気をさらに加熱して、100℃を越える高温状態にしたものであり、酸素がほとんど含まれていないので不活性であり、それでいて常圧過熱水蒸気の単位容積の熱量は、同温度の熱風空気の約4倍あると言われ、温度も500℃以上に容易に出来るものである。したがって、この常圧過熱水蒸気発生装置45は、常圧過熱水蒸気を発生出来るものであれば特に限定がないが、例えば、特開2004−251605に示す電磁誘導式のものが採用される。  The sterilizing unit 4B includes a superheated steam chamber 42 and a steam chamber conveyor 43 that travels in the chamber. The superheated steam chamber 42 is connected to a boiler 44 via a normal pressure superheated steam generator 45. This normal pressure superheated steam generator 45 generates normal pressure superheated steam, and this normal pressure superheated steam further heats saturated steam from a normal boiler, for example, the boiler 44, to 100 ° C. It is inactive because it contains almost no oxygen, and it is said that the unit volume of atmospheric superheated steam is about four times that of hot air at the same temperature. It can be easily done at 500 ° C. or higher. Accordingly, the normal pressure superheated steam generator 45 is not particularly limited as long as it can generate normal pressure superheated steam, but for example, an electromagnetic induction type apparatus disclosed in JP-A-2004-251605 is adopted.

以上のような構成の洗浄殺菌部4は、米定量供給機30から定量的に供給した米に対して、まず、エアー吹出管25からエアーを吹き付けると共に吸引して粗洗浄し、次に、霧吹出管26の噴霧ノズル36から霧を吹き付けると共に吸引して洗浄して、さらに、エアー吹出管27からエアーを吹き付けると共に吸引して仕上げ洗浄を行うことになる。洗浄を終了した米は、前記殺菌部4Bの過熱蒸気室42内の蒸気室コンベアー43上に供給され、走行中に常圧過熱水蒸気発生装置45からの常圧過熱水蒸気により米が殺菌され、品温も上昇し、前記吸水部5に送られる。なお、上記洗浄殺菌部4は、殺菌部4Bを省略して、洗浄部4Aのエアー吹出管25、霧吹出管26及びエアー吹出管27に常圧過熱水蒸気発生装置45を接続し、米に常圧過熱水蒸気を吹き付けるだけでも、米の洗浄殺菌が可能となる。したがって、米の種類や、麦やそばなど他の穀物の場合、この方式をとる方がベターであることもあるので、この方式を排除するものではない。  The cleaning and sterilizing unit 4 having the above-described configuration first performs rough cleaning by blowing and sucking air from the air blowing pipe 25 to the rice quantitatively supplied from the rice fixed quantity feeder 30, and then Fog is blown from the spray nozzle 36 of the outlet pipe 26 and suctioned for cleaning, and further, air is blown from the air outlet pipe 27 and sucked for finishing cleaning. The rice after washing is supplied onto the steam chamber conveyor 43 in the superheated steam chamber 42 of the sterilization unit 4B, and the rice is sterilized by normal pressure superheated steam from the normal pressure superheated steam generator 45 during running. The temperature also rises and is sent to the water absorption part 5. The cleaning and sterilizing unit 4 omits the sterilizing unit 4B, and connects the atmospheric pressure superheated steam generator 45 to the air blowing pipe 25, the mist blowing pipe 26 and the air blowing pipe 27 of the washing unit 4A so The rice can be washed and sterilized only by spraying superheated steam. Therefore, in the case of other cereals such as rice types and wheat and buckwheat, this method may be better, so this method is not excluded.

前記吸水部5は、30℃〜48℃の湯50に洗浄殺菌後の米をさらし、吸水させるものであり、水槽51に張った30℃〜48℃の湯50内を走行するネットコンベア52により構成する。すなわち、洗浄殺菌部4からの洗浄殺菌後の米をネットコンベア52で受け、このネットコンベア52が湯50中を走行する20秒間〜10分間で浸漬して、その間に米に吸水させ、さらに、ネットコンベア52が湯50から出て蒸し機8に米を投入する間に吸引部52aを通過させ水切りをするものである。米は上述の方法で洗浄殺菌され且つ品温も上昇しているから、30℃〜48℃の湯50の温度を下げることなく、短時間の浸漬で吸水し、しかも米を洗浄殺菌してあるから水槽51内での菌の繁殖がなく、吸水して減った分の湯50を水槽51内に供給してやれば良い。したがって、この方式では、120分間滞留させ得るだけの容量のタンクが2基必要になるようなことがない。なお、この吸水部5は30℃〜48℃の湯50内に米を浸漬して吸水させたが、米に30℃〜48℃の湯50をシャワーリングして吸水させても、差し支えない。  The water-absorbing part 5 exposes the washed and sterilized rice to hot water 50 at 30 ° C. to 48 ° C. to absorb the water, and a net conveyor 52 running in the hot water 50 at 30 ° C. to 48 ° C. stretched on the water tank 51. Constitute. That is, the rice after washing and sterilization from the washing and sterilizing unit 4 is received by the net conveyor 52, and the net conveyor 52 is immersed in the hot water 50 for 20 seconds to 10 minutes, during which time the rice absorbs water, While the net conveyor 52 comes out of the hot water 50 and puts rice into the steamer 8, it passes through the suction part 52a to drain water. The rice has been washed and sterilized by the above-mentioned method and the product temperature has risen, so the water is absorbed in a short period of time without lowering the temperature of the hot water 50 of 30 ° C. to 48 ° C., and the rice is washed and sterilized. Therefore, there is no propagation of bacteria in the water tank 51, and the water 50 that has been absorbed and reduced can be supplied into the water tank 51. Therefore, this system does not require two tanks having a capacity capable of retaining for 120 minutes. In addition, although this water absorption part 5 dipped the rice in the hot water 50 of 30 degreeC-48 degreeC and made it water-absorb, even if it showers the hot water 50 of 30 degreeC-48 degreeC on the rice and water-absorbed, it does not interfere.

前記蒸し機8は、下部がV字状なったタンク6内の底部に定量フィーダー7を設け、この定量フィーダー7はモータ7aに直結し、タンク6の側面には定量フィーダー7の排出管60が設けられている。この排出管60は、水平に設けた直管61とその先端に曲管62を取り付けてなる。そして、このタンク6は、そのV字状になった底板6a及び側板6bの外側を板にて覆い蒸気室63を形成し、さらに、タンク6内にある定量フィーダー7の上方に蒸気吹出管64を設けている。これら蒸気室63及び蒸気吹出管64は前記ボイラー43に直結している。このボイラー43は、タンク6及び前記常圧過熱水蒸気発生装置44内に0.25kg/cm〜1.5kg/cmの飽和水蒸気を吹き込むことができるものが選択される。The steamer 8 is provided with a metering feeder 7 at the bottom of the tank 6 having a V-shaped lower part. The metering feeder 7 is directly connected to the motor 7 a, and a discharge pipe 60 of the metering feeder 7 is provided on the side of the tank 6. Is provided. The discharge pipe 60 is composed of a straight pipe 61 provided horizontally and a curved pipe 62 attached to the tip thereof. The tank 6 covers the outside of the V-shaped bottom plate 6 a and side plate 6 b with a plate to form a steam chamber 63, and further, a steam outlet pipe 64 above the metering feeder 7 in the tank 6. Is provided. The steam chamber 63 and the steam outlet pipe 64 are directly connected to the boiler 43. The boiler 43 is selected to be able to blow 0.25 kg / cm 2 to 1.5 kg / cm 2 of saturated steam into the tank 6 and the atmospheric superheated steam generator 44.

前記計量機9は、図6に示すように、蒸し機8の排出管60からの蒸し米を一旦受け入れるホッパー65と、このホッパー65下に取り付けた予備ほぐし機66と、この予備ほぐし機66を通過したあとの蒸し米を計量する計量部67とからなる。この計量機9は、蒸し機8の排出管60から定量フィーダー7によりほぼ定量的に送られてくる蒸し米をホッパー65にて受け入れ、予備ほぐし機66の2本のパドル66aとほぐしドラム66bとにより予備ほぐしを行い、さらに計量部67にて予め定めた量を計量すると、排出管60からの蒸し米の供給を一時的に止め、一旦袋68に計量した量の蒸し米を入れる。  As shown in FIG. 6, the weighing machine 9 includes a hopper 65 that temporarily receives steamed rice from the discharge pipe 60 of the steamer 8, a preliminary loosening machine 66 attached under the hopper 65, and the preliminary loosening machine 66. It comprises a measuring unit 67 for measuring the steamed rice after passing. The weighing machine 9 receives the steamed rice, which is sent almost quantitatively from the discharge pipe 60 of the steamer 8 by the quantitative feeder 7, by the hopper 65, and includes two paddles 66a and a loosening drum 66b of the preliminary loosening machine 66. When a predetermined amount is weighed by the weighing unit 67, the supply of the steamed rice from the discharge pipe 60 is temporarily stopped, and the amount of the steamed rice is once put in the bag 68.

前記真空冷却機11は、複数の容器10として少なくとも4個有している。これら容器10には、自動的に開閉し密封できるフタが設けられ、順次以下に示す工程70、71、73、75を踏み循環するようになっている。第1の工程70は、容器10のフタを開いて、蒸し米を収容した袋68を開封のままの状態で容器10内に入れる工程である。第2の工程71は、容器10のフタを閉じて密封し、真空発生機72に接続して690mmHg以上の真空状態を10秒間〜30秒間保持するようにした工程である。第3の工程73は、無菌エアー発生機74に接続して容器10内を大気圧にすると共に、容器10内に設けたシール機(図示せず)により袋68をシールする工程である。第4の工程75は、容器10を開いて袋68を取り出し搬送コンベアー76に載せる工程である。
なお、前記計量機9の計量部67から出た蒸し米を袋68に入れないで、そのまま容器10に入れても良い。この場合、後述の熟成ヤード18は、外部汚染が無く、蒸し米に残留した菌による繁殖がないような対策、例えば、無菌室や低温室とする必要がある。そして、得られた熟成米は、直接乾燥部13に送られ、あるいは後述の本ほぐし機19を経由して乾燥部13に送られることになる。
The vacuum cooler 11 has at least four containers 10 as a plurality of containers 10. These containers 10 are provided with a lid that can be automatically opened and closed and sealed so that the steps 70, 71, 73, and 75 shown below are sequentially circulated. The first step 70 is a step of opening the lid of the container 10 and putting the bag 68 containing the steamed rice into the container 10 in an opened state. The second step 71 is a step in which the lid of the container 10 is closed and sealed, and connected to the vacuum generator 72 so that a vacuum state of 690 mmHg or more is maintained for 10 seconds to 30 seconds. The third step 73 is a step of connecting the sterilized air generator 74 to bring the inside of the container 10 to atmospheric pressure and sealing the bag 68 by a sealing machine (not shown) provided in the container 10. The fourth step 75 is a step of opening the container 10, taking out the bag 68 and placing it on the transport conveyor 76.
Note that the steamed rice from the weighing unit 67 of the weighing machine 9 may be put in the container 10 as it is without being put in the bag 68. In this case, the maturation yard 18 described later needs to be a measure that is free from external contamination and does not propagate by bacteria remaining in the steamed rice, for example, a sterile room or a cold room. And the obtained matured rice is sent to the drying part 13 directly, or is sent to the drying part 13 via the below-mentioned unwinding machine 19.

上記真空冷却機11の冷却負荷を軽減するために、すなわち、真空発生機72の容量を小さくするために、排出管60から排出した蒸し米を計量して袋68に入れるまでの間に、バルブ77を開いて前述の無菌エアー発生機74から無菌エアーを蒸し米に吹き付けるのが良い。このようにすることにより、排出管60から排出した直後の蒸し米は98℃ぐらいであるが、直ちに80℃〜70℃に低下させることができる。  In order to reduce the cooling load of the vacuum cooler 11, that is, to reduce the capacity of the vacuum generator 72, the steamed rice discharged from the discharge pipe 60 is measured before being put into the bag 68. 77 is opened and aseptic air is preferably sprayed onto the steamed rice from the aforementioned aseptic air generator 74. By doing in this way, the steamed rice immediately after discharging | emitting from the discharge pipe 60 is about 98 degreeC, However, It can reduce to 80 to 70 degreeC immediately.

前記熟成ほぐし部12は、搬送コンベアー76により搬送された袋68入りの20℃程の蒸し米を、常温にて24時間〜48時間放置しアルファー化した米澱粉を熟成させる熟成ヤード18と、この袋入りの熟成米をそのまま本ほぐしを行い、単粒化した状態にする本ほぐし機19と、からなる。この熟成ヤード18は、蒸し米が袋68に入っているから常温でも良く、夏場などで著しく気温が上昇しない倉庫であれば、その役割を果たすことができる。この熟成ヤード18において、袋68入り熟成米は、アルファー化状態、すなわち、通常の炊き上がった状態である澱粉分子が水分子と結合しそれらを媒介にして互いに連なった状態で安定化し、離しょう現象が生じない状態となっている。この袋68入り熟成米は、予備ほぐしされてはいるものの、米粒子が付着して塊状態になっている。  The maturing loosening unit 12 includes a maturing yard 18 for maturing rice starch that has been allowed to stand for 24 to 48 hours at room temperature for 24 hours to 48 hours in steamed rice in a bag 68 that is transported by a transport conveyor 76, and this This unraveling machine 19 is used to unravel the bagged ripened rice as it is to make it into a single grain. The maturing yard 18 may be at room temperature because the steamed rice is contained in the bag 68, and can serve as a warehouse where the temperature does not rise significantly in summer or the like. In this ripening yard 18, the ripened rice in the bag 68 is stabilized and separated in a pregelatinized state, that is, in a state where starch molecules in a normal cooked state bind to water molecules and are linked to each other through them. The phenomenon does not occur. The ripened rice in the bag 68 is preliminarily loosened, but the rice particles are attached to form a lump.

そこで、前記本ほぐし機19により、袋68入り熟成米は更にほぐされ、単粒化した状態とされる。すなわち、この本ほぐし機19は、上部コンベアー78と下部コンベアー79とからなり、これら双方のコンベアー78及び79のローラ78a及び79aが千鳥状に配置されている。これらコンベアー78及び79のローラ78a及び79aの間に袋68を通すことにより、塊状の熟成米は既に予備ほぐしされているので米粒子の付着力が弱く、この本ほぐしにより更にほぐされて、ほぼ完全に単粒化し、通常の生米とほとんど変わらないような状態になり、袋開封機80に送られる。  Therefore, the ripened rice in the bag 68 is further loosened by the present loosening machine 19 and is made into a single grain state. That is, the present unraveling machine 19 includes an upper conveyor 78 and a lower conveyor 79, and the rollers 78a and 79a of both the conveyors 78 and 79 are arranged in a staggered manner. By passing the bag 68 between the rollers 78a and 79a of the conveyors 78 and 79, the agglomerated ripened rice has already been preliminarily loosened, so that the adhesion of the rice particles is weak, and this loosening is further loosened. It is made into a single grain and becomes almost the same as ordinary raw rice, and is sent to the bag opening machine 80.

この袋開封機80は、袋68を開封して単粒化した熟成米を取り出すためのもので、その取り出された熟成米は前記乾燥部13の受入タンク81に投入される。  The bag opening machine 80 is used to take out the matured rice that has been made into a single grain by opening the bag 68, and the matured rice that has been taken out is put into the receiving tank 81 of the drying unit 13.

この乾燥部13は、わずかに傾斜しゆるやかに回転する円筒体82と、円筒体82の内壁に設けられた掻上翼83とからなるロータリー乾燥機であり、この円筒体82は前記常圧過熱水蒸気発生装置45に接続している。熟成米は、受入タンク81から円筒体82の上端側に供給され、円筒体82のゆるやかな回転につれて、掻上翼83により掻き上げられて落下するという運動を繰り返しながら、円筒体82の下端側にへと移動する過程で、円筒体82内を流れる常圧過熱水蒸気により、粉砕条件や米粉の使用目的などに鑑み、予め設定された水分値まで乾燥されて、前記粉化部14に投入される。なお、この乾燥部13は、特に限定がなく、過熱蒸気室とこの中を走行する蒸気室コンベアーとからなるバンド乾燥機であっても良く、この過熱蒸気室は常圧過熱水蒸気発生装置45に接続し、熟成米は、蒸気室コンベアー上に載せられ過熱蒸気室内を走行する過程で、予め設定された水分値まで乾燥される。  The drying unit 13 is a rotary dryer that includes a cylindrical body 82 that is slightly inclined and rotates gently, and a scraper blade 83 that is provided on the inner wall of the cylindrical body 82. It is connected to the steam generator 45. Aged rice is supplied from the receiving tank 81 to the upper end side of the cylindrical body 82, and as the cylindrical body 82 rotates slowly, it is scraped up and dropped by the raising blade 83, and the lower end side of the cylindrical body 82 In the process of moving to, the atmospheric pressure superheated steam flowing in the cylindrical body 82 is dried to a preset moisture value in view of the pulverization conditions and the purpose of use of rice flour, and put into the pulverizing section 14. The The drying unit 13 is not particularly limited, and may be a band dryer including a superheated steam chamber and a steam chamber conveyor that travels inside the superheated steam chamber. Connected and matured rice is dried to a preset moisture value in the process of being placed on the steam chamber conveyor and traveling in the superheated steam chamber.

この粉化部14は、米粉の使用目的などに鑑み、乾燥米を予め設定された粒度に粉砕するものであり、従来公知の粉砕機、例えば、ロール式粉砕機、衝撃式粉砕機などが採用される。粉砕して得られた米粉は、直ちに袋84に詰められ、米粉製品85となり、この米粉製品85は製品ヤード86に積まれる。  In consideration of the purpose of use of the rice flour, the pulverizing unit 14 pulverizes dried rice to a predetermined particle size, and a conventionally known pulverizer such as a roll pulverizer or an impact pulverizer is employed. Is done. The rice flour obtained by pulverization is immediately packed in a bag 84 to become a rice flour product 85, and this rice flour product 85 is stacked in a product yard 86.

次に、上記構成になる米粉の製造装置1により、その製造方法1Aを説明する。
生米が貯留されている貯留タンク2の下部にあるロータリーバルブ15を開いて搬送装置16を作動させ、さらにバルブ17を開いて、洗浄殺菌部4の洗浄部4Aにおける米定量供給機30の受入タンク31に米を供給する。
Next, the manufacturing method 1A is demonstrated with the rice flour manufacturing apparatus 1 which becomes the said structure.
Opening of the rotary valve 15 at the lower part of the storage tank 2 in which raw rice is stored opens the conveying device 16, opens the valve 17, and accepts the rice fixed quantity feeder 30 in the cleaning unit 4 </ b> A of the cleaning sterilization unit 4. Rice is supplied to the tank 31.

受入タンク31に供給された米Rを振動機33により、通路32を振動させて通路32から洗浄部4Aの加圧室28に定量的に供給する。加圧室28に入った米Rに、ブロワー34からのエアーをエアー吹出管25により平均的に吹き付け、米Rの米付着物40のうち比較的付着力の弱い米付着物40を粗取りして粗洗浄する。次に、霧発生器35及び霧吹出管26の噴霧ノズル36からの霧を米に吹き付けると共に吸引して洗浄し、さらに、ブロワー34からのエアーをエアー吹出管27により米Rに平均的に吹き付けて、米付着物40をさらに除去して仕上げ洗浄を行い、洗浄を終了させる。なお、同時に減圧室29を真空ポンプ37により減圧しているから、エアー及び霧と共に、米付着物40及び米付着物臭はネット3を通過して減圧室29を経由して米付着物除去タンク38内に入り、ここで米付着物40は分離されてロータリーバルブ39によりトレー41に落とされ回収される。  The rice R supplied to the receiving tank 31 is oscillated by the vibrator 33 to vibrate the passage 32 and is quantitatively supplied from the passage 32 to the pressurizing chamber 28 of the cleaning unit 4A. Air from the blower 34 is averagely blown to the rice R that has entered the pressurizing chamber 28 by the air blowing pipe 25, and the rice deposit 40 having relatively weak adhesion is roughly removed from the rice deposit 40 of the rice R. Wash roughly. Next, the mist from the mist generator 35 and the spray nozzle 36 of the mist blowing pipe 26 is blown onto the rice and washed by suction, and air from the blower 34 is blown on the rice R by the air blowing pipe 27 on the average. Then, the rice deposit 40 is further removed to perform final cleaning, and the cleaning is terminated. At the same time, since the decompression chamber 29 is decompressed by the vacuum pump 37, the rice deposit 40 and the rice deposit odor pass through the net 3 along with the air and mist and pass through the decompression chamber 29 to the rice deposit removal tank. 38, the rice deposit 40 is separated and dropped onto the tray 41 by the rotary valve 39 and collected.

そして、洗浄を終了した米Rは、前記殺菌部4Bの過熱蒸気室42内の蒸気室コンベアー43上に供給される。一方、ボイラー44からの飽和水蒸気を、常圧過熱水蒸気発生装置45に通して、100℃〜350℃の常圧過熱水蒸気とし、この常圧過熱水蒸気を過熱蒸気室42内に送り、蒸気室コンベアー43により走行中の米Rを殺菌し且つその品温も上昇させて、殺菌を付加した洗浄工程1Bが終了する。なお、この常圧過熱水蒸気は飽和水蒸気と異なり、熱量が高いので常圧過熱水蒸気中の水が凝結して米Rに付着するようなことがなく、米Rがサラサラ状態を保持して殺菌されつつ過熱蒸気室42内を通過してゆく。そして、洗浄殺菌を終了した米Rは、前記吸水部5の水槽51内のネットコンベアー52上に送られる。  And the rice R which complete | finished washing | cleaning is supplied on the steam chamber conveyor 43 in the superheated steam chamber 42 of the said sterilization part 4B. On the other hand, saturated steam from the boiler 44 is passed through a normal pressure superheated steam generator 45 to form normal pressure superheated steam at 100 ° C. to 350 ° C., and this normal pressure superheated steam is sent into the superheated steam chamber 42, and a steam chamber conveyor 43, the running rice R is sterilized and its product temperature is raised, and the cleaning process 1B with sterilization is completed. Note that this atmospheric superheated steam is different from saturated water vapor in that it has a high amount of heat, so that the water in the atmospheric superheated steam does not condense and adhere to the rice R, and the rice R is sterilized while maintaining a smooth state. While passing through the superheated steam chamber 42. And the rice R which finished | finished washing | cleaning sterilization is sent on the net conveyor 52 in the water tank 51 of the said water absorption part 5. FIG.

ネットコンベアー52は、30℃〜48℃の湯50の入った水槽51内を20秒間〜10分間程かけてゆっくり走行し、この浸漬時間内で米Rに吸水させ、さらに、ネットコンベア52が湯50から出て蒸し機8に米Rを投入する間に、適宜吸引部52aに真空配管などを接続して吸引し水切りをすることで、吸水工程1Cが終了する。なお、米Rは、洗浄殺菌部4で洗浄殺菌され且つ品温も上昇しているから、湯50の温度を下げることなく、短時間の浸漬で充分吸水し、しかも水槽51内での菌の繁殖がなく、吸水して減った分の湯50を水槽51内に供給すれば良いことになる。  The net conveyor 52 travels slowly in a water tank 51 containing hot water 50 at 30 ° C. to 48 ° C. for about 20 seconds to 10 minutes, and the rice R absorbs water within this dipping time. While taking out the rice R into the steamer 8 from 50, the suction step 52a is appropriately connected to a suction pipe 52a for suction and draining, thereby completing the water absorption step 1C. The rice R is washed and sterilized in the washing and sterilizing section 4 and the product temperature is also raised. Therefore, the rice R absorbs water sufficiently by dipping in a short time without lowering the temperature of the hot water 50, and the bacteria R in the water tank 51 is also absorbed. There is no breeding, and it is only necessary to supply the water 50 that has been absorbed and reduced in the water tank 51.

次に、ネットコンベアー52から蒸し機8のタンク6内に一定量の米Rが投入されたら、ボイラー43からタンク6の外側にある蒸気室63及び蒸気吹出管64に0.25kg/cm〜1.5kg/cmの飽和水蒸気を送り込み、タンク6の底板6a及び側板6bの多数の孔6c並びに蒸気吹出管34から飽和水蒸気を吹き出し、米を蒸す。この間、定量フィーダー7を稼働させると、排出管60から予め設定した蒸し具合、すなわち、予め設定したアルファー化度まで蒸していない米を排出することになるので、タンク6内の米を攪拌する程度に定量フィーダー7を間欠的に稼働させさせたり、正逆回転させたりして予め設定した蒸し具合の蒸し米になるまで、排出管60から米Rを排出しないようにしている。Next, when a certain amount of rice R is put into the tank 6 of the steamer 8 from the net conveyor 52, the steam chamber 63 and the steam outlet pipe 64 outside the tank 6 are supplied from the boiler 43 to 0.25 kg / cm 2 . Saturated water vapor of 1.5 kg / cm 2 is fed in, steam is blown out from the numerous holes 6c of the bottom plate 6a and side plate 6b of the tank 6 and the steam blowing pipe 34, and the rice is steamed. During this time, when the quantitative feeder 7 is operated, the steaming condition set in advance from the discharge pipe 60, that is, the rice that has not been steamed to the pre-set alpha degree is discharged, so that the rice in the tank 6 is stirred. The rice feeder R is prevented from being discharged from the discharge pipe 60 until the metering feeder 7 is intermittently operated or rotated forward and backward until the steamed rice has a preset steaming condition.

蒸し機8内で米Rが、予め設定した蒸し具合まで蒸し上がったら、定常的な定量フィーダー7の運転に入る。米Rが蒸し機8のタンク6内に投入され排出管60から排出されるまでの時間、すなわち、予め設定したアルファー化度まで蒸し上がる所定の時間滞留するように設定する。この滞留時間は、米Rの浸漬時間、換言すれば、米Rに水がどの程度吸収しているか、蒸気圧、米澱粉のアルファー化度をどの程度にするか、などのファクターにより大きく変化する。いずれにしても、米粉の使用目的に合わせたアルファー化度になるように蒸し時間及び蒸気圧を調整する。  When the rice R is steamed to a preset steaming condition in the steamer 8, the operation of the constant quantitative feeder 7 is started. The time until the rice R is introduced into the tank 6 of the steamer 8 and discharged from the discharge pipe 60, that is, a predetermined time during which the rice R is steamed to a preset alpha degree is set. This residence time varies greatly depending on factors such as the soaking time of rice R, in other words, how much water is absorbed in rice R, the vapor pressure, and the degree of alpha conversion of rice starch. . In any case, the steaming time and the steam pressure are adjusted so that the degree of pregelatinization according to the intended purpose of the rice flour is obtained.

定常運転に入った蒸し機8の排出管60から、蒸し米が計量機9のホッパー65に投入されるが、排出管60の先端が曲管62になっているから、排出管60内に蒸し米が充満した状態になり、蒸し米がかなり高い精度で定量的にホッパー65に投入され、蒸し工程1Dが終了することになる。そして、ホッパー65下の予備ほぐし機66により蒸し米を予備ほぐしする。この予備ほぐしは、回転している2本のパドル66aの間を蒸し米が通り、さらに、回転しているドラム66bを通過することにより実施され、蒸し米は一旦バラける。予備ほぐしにより一旦バラけた蒸し米は、計量部67により計量が行われる。すなわち、計量部67が蒸し米を予め定めた量に計量すると、排出管60からの蒸し米の供給を一時的に止めると共に、計量部67の下部を開き計量した量の蒸し米を袋68に入れる。  Steamed rice is put into the hopper 65 of the weighing machine 9 from the discharge pipe 60 of the steamer 8 which has entered the steady operation, but since the tip of the discharge pipe 60 is a curved pipe 62, the steamed rice is steamed into the discharge pipe 60. The rice is filled, and the steamed rice is quantitatively introduced into the hopper 65 with considerably high accuracy, and the steaming process 1D is completed. Then, the steamed rice is preliminarily loosened by the preliminary loosening machine 66 under the hopper 65. This preliminary loosening is carried out when steamed rice passes between the two rotating paddles 66a and further passes through the rotating drum 66b, and the steamed rice is once broken. The steamed rice once broken by the preliminary loosening is measured by the measuring unit 67. That is, when the measuring unit 67 measures the steamed rice to a predetermined amount, the supply of the steamed rice from the discharge pipe 60 is temporarily stopped, and the lower part of the measuring unit 67 is opened to measure the amount of steamed rice in the bag 68. Put in.

この蒸し米入りの袋68は、その口を開いたまま前記真空冷却機11の第1の工程70の位置にある容器10内にセットされ、その一方で計量部67の下方に空の袋68がセットされる。さらに、排出管60から排出した蒸し米に、バルブ77を開いて無菌エアー発生機74から無菌エアーを吹き付ければ、排出した直後の98℃程度の蒸し米の温度を直ちに80℃〜70℃に低下させ得るから、真空冷却機11の冷却負荷を大幅に軽減することができる。  The bag 68 containing the steamed rice is set in the container 10 at the position of the first step 70 of the vacuum cooler 11 with its mouth open, while the empty bag 68 is placed below the measuring unit 67. Is set. Furthermore, if the valve 77 is opened and the sterilized air is blown from the sterilized air generator 74 to the steamed rice discharged from the discharge pipe 60, the temperature of the steamed rice at about 98 ° C immediately after the discharge is immediately increased to 80 ° C to 70 ° C. Since it can reduce, the cooling load of the vacuum cooler 11 can be reduced significantly.

次に、真空冷却機11の第1の工程70の位置にある容器10は、フタを閉じ第2の工程71に進み、ここで真空発生機72に接続して減圧して行き蒸し米の温度を急速に下げ、690mmHg以上の真空状態を10秒間〜30秒間保持することができるようになると、蒸し米の温度は常温、約20℃程になる。  Next, the container 10 at the position of the first step 70 of the vacuum cooler 11 closes the lid and proceeds to the second step 71, where it is connected to the vacuum generator 72 to reduce the pressure, and the temperature of the steamed rice When the temperature is lowered rapidly and a vacuum state of 690 mmHg or more can be maintained for 10 seconds to 30 seconds, the temperature of the steamed rice becomes about 20 ° C. at room temperature.

容器10が第3の工程73に進むと、無菌エアー発生機74により容器10内に無菌エアーを送り大気圧にしてから、容器10内に設けたシール機(図示せず)により袋68をシールして密封する。さらに、容器10は第4の工程75に進み、容器10のフタを開いて袋68を取り出し搬送コンベアー76に載せ、熟成ほぐし部12の熟成ヤード18に袋68を搬送することで、冷却工程1Gが終了する。  When the container 10 proceeds to the third step 73, the sterilized air generator 74 sends sterilized air into the container 10 to bring it to atmospheric pressure, and then the bag 68 is sealed by a sealing machine (not shown) provided in the container 10. And seal. Further, the container 10 proceeds to the fourth step 75, the lid of the container 10 is opened, the bag 68 is taken out and placed on the transport conveyor 76, and the bag 68 is transported to the aging yard 18 of the aging loosening unit 12, thereby cooling step 1G. Ends.

この熟成ヤード18にて、袋68を常温で24時間〜48時間放置し、その間に袋68内の蒸し米は熟成し、米澱粉のアルファー化状態が安定化すると共に、予備ほぐしにより一旦バラけた米粒同士が再び付着して塊となる。したがって、本ほぐし機19の上部コンベアー78及び下部コンベアー79のローラ78a及び79aの間に袋68を通すことにより、塊状のアルファー化処理した熟成米はほぐされて、ほぼ完全に単粒化し、通常の生米とほとんど変わらないような状態になり、熟成工程1Hが終了する。  In this ripening yard 18, the bag 68 is left at room temperature for 24 to 48 hours, during which steamed rice in the bag 68 ripens, stabilizes the alpha state of the rice starch, and is temporarily broken by preliminary loosening. Rice grains adhere again to form a lump. Therefore, by passing the bag 68 between the rollers 78a and 79a of the upper conveyor 78 and the lower conveyor 79 of the present loosening machine 19, the agglomerated ripened rice is loosened and almost completely made into a single grain. Thus, the ripening process 1H is completed.

袋68詰めの単粒化した熟成米は、開封機80に送られ袋68が開封されて、袋68から前記乾燥部13の受入タンク81に投入される。そして、受入タンク81から単粒化した熟成米が上端側の円筒体82内に供給され、熟成米が掻上機83により掻き上げられて落下するという運動を繰り返しながら、円筒体82の下端側にへと移動する間に、円筒体82内を流れる常圧過熱水蒸気により、熟成米は予め設定された水分値まで乾燥されて、前記粉化部14に投入され、乾燥工程1Eが終了する。なお、熱含量の高い(同温度の熱風空気の約4倍)常圧過熱水蒸気を使用して熟成米を乾燥するから、乾燥が早く、その上無酸素状態であるため米に含有するビタミンや酵素などにもあまり影響を与えず、殺菌効果も高い。  The ripened ripened rice packed in the bag 68 is sent to the opening machine 80, the bag 68 is opened, and the bag 68 is put into the receiving tank 81 of the drying unit 13. Then, the ripened rice singulated from the receiving tank 81 is supplied into the cylinder 82 on the upper end side, and the aged rice is scraped up by the scraper 83 and dropped, and the lower end side of the cylinder 82 is repeated. In the meantime, the aged rice is dried to a preset moisture value by the atmospheric superheated steam flowing in the cylindrical body 82 and put into the pulverizing section 14, and the drying step 1E is completed. Since mature rice is dried using atmospheric superheated steam with a high heat content (about 4 times that of hot air at the same temperature), it is dry quickly and oxygen-free. It has little effect on enzymes and has a high bactericidal effect.

乾燥米は、粉化部14に送られて、予め設定された粒度に粉砕されて、得られた米粉は直ちに袋84に詰められ、米粉製品85となる。この米粉製品85は、製品ヤード86に積まれ、粉化工程1Fは終了する。  The dried rice is sent to the pulverizing section 14 and pulverized to a preset particle size, and the obtained rice flour is immediately packed in the bag 84 to become a rice flour product 85. The rice flour product 85 is stacked in the product yard 86, and the powdering process 1F is completed.

図7は図1に示す米粉の製造方法における乾燥工程の直前に平板化工程を付加したフロシート図である。図面において、米粉の製造方法1Aaにおける平板化工程1Jは、蒸し工程1Dからの蒸し米を潰して板状にする場合と、熟成工程1Hからの熟成米を潰して板状にする場合とがある。いずれの場合も、粒状の米を板状にすることで薄くして、次の乾燥工程1Eでの乾燥効率を向上させようとする工程である。  FIG. 7 is a flow sheet diagram in which a flattening step is added immediately before the drying step in the method for producing rice flour shown in FIG. In the drawing, the flattening step 1J in the rice flour production method 1Aa may be a case where the steamed rice from the steaming step 1D is crushed into a plate shape, or a case where the aged rice from the aging step 1H is crushed into a plate shape. . In any case, the granular rice is made thin by making it into a plate shape, and is a step for improving the drying efficiency in the next drying step 1E.

次に、上記した平板化工程を付加した米粉の製造方法1Aaを具体的に実施する米粉の製造装置について説明する。図8は蒸し工程1Dからの蒸し米を潰して板状にする場合の米粉の製造方法を具体化した製造装置のフロシート図であり、図9は熟成工程1Hからの熟成米を潰して板状にする場合の米粉の製造方法を具体化する製造装置のフロシート図である。  Next, a rice flour producing apparatus that specifically implements the rice flour producing method 1Aa to which the above-described flattening step is added will be described. FIG. 8 is a flow sheet diagram of a production apparatus that embodies a method for producing rice flour when the steamed rice from the steaming step 1D is crushed into a plate shape, and FIG. 9 is a plate shape by crushing the ripened rice from the aging step 1H. It is a flow sheet figure of the manufacturing apparatus which materializes the manufacturing method of the rice flour in the case of making.

図8において、蒸し機8の排出管60からの蒸し米をホッパー65aに受け入れてから平板加工機90に供給される。この平板加工機90は、蒸気室コンベアー91の駆動機92により走行するステンレス製の無端ベルト93を挟んで設置した押圧ロール94及び受圧ロール95からなる。平板加工機90の無端ベルト93上に供給された蒸し米は、押圧ロール94と受圧ロール95との間を通過することで板状にされて、平板化工程1Jが終了する。無端ベルト93上の板状となった蒸し米はそのまま乾燥部13aに送られる。この乾燥部13aは、過熱蒸気室96と、この中を走行する上述の蒸気室コンベアー91とからなるバンド乾燥機であり、この過熱蒸気室96は常圧過熱水蒸気発生装置45に接続している。板状の蒸し米は、無端ベルト93上に載せられまま過熱蒸気室96内を走行する過程で、過熱蒸気室96内を流れる常圧過熱蒸気により、予め設定された水分値まで乾燥されて乾燥工程1Eが終了し、前記粉化部14に投入される。  In FIG. 8, the steamed rice from the discharge pipe 60 of the steamer 8 is received by the hopper 65a and then supplied to the flat plate processing machine 90. The flat plate processing machine 90 includes a pressing roll 94 and a pressure receiving roll 95 that are installed with a stainless endless belt 93 that is driven by a drive unit 92 of a steam chamber conveyor 91 interposed therebetween. The steamed rice supplied onto the endless belt 93 of the flat plate processing machine 90 is made into a plate shape by passing between the pressing roll 94 and the pressure receiving roll 95, and the flattening step 1J is completed. The steamed rice in the form of a plate on the endless belt 93 is sent to the drying unit 13a as it is. The drying unit 13 a is a band dryer including a superheated steam chamber 96 and the above-described steam chamber conveyor 91 that travels in the superheated steam chamber 96. The superheated steam chamber 96 is connected to the atmospheric pressure superheated steam generator 45. . The plate-shaped steamed rice is dried to a preset moisture value by normal pressure superheated steam flowing in the superheated steam chamber 96 in the process of running in the superheated steam chamber 96 while being placed on the endless belt 93. Step 1E is finished and charged into the pulverizing section 14.

図9において、袋開封機80により開封された熟成米は、一旦受入タンク81に投入されてから、平板加工機90の無端ベルト93上に供給される。無端ベルト93上の熟成米は、上記の蒸し米の場合と同様に、押圧ロール94と受圧ロール95との間を通過することで板状にされ、さらに、無端ベルト93上の板状の熟成米はそのまま乾燥部13aに送られ、過熱蒸気室96内を流れる常圧過熱蒸気により、予め設定された水分値まで乾燥されて、平板化工程1J及び乾燥工程1Eが終了し、前記粉化部14に投入される。  In FIG. 9, the aged rice opened by the bag opening machine 80 is once put into the receiving tank 81 and then supplied onto the endless belt 93 of the flat plate processing machine 90. The aged rice on the endless belt 93 is formed into a plate shape by passing between the pressing roll 94 and the pressure receiving roll 95 as in the case of the above steamed rice, and further, the aged plate shape on the endless belt 93 is formed. The rice is sent to the drying unit 13a as it is, and is dried to a preset moisture value by the atmospheric superheated steam flowing in the superheated steam chamber 96, and the flattening step 1J and the drying step 1E are finished, and the powdering unit 14.

以上、本発明を実施するための最良の形態を説明したが、具体的な構成はこれに限定されず、例えば、米についてのみ説明したが、さらに麦、そばなどの穀物についても適用出来ることは言うまでもなく、本発明の要旨を逸脱しない範囲での変更は適宜可能であることは理解されるべきである。  Although the best mode for carrying out the present invention has been described above, the specific configuration is not limited to this. For example, only rice has been described, but it can also be applied to grains such as wheat and buckwheat. Needless to say, it should be understood that modifications can be made as appropriate without departing from the scope of the present invention.

本発明の米粉の製造方法及びその装置は、廃水処理施設も含めた設備構成の小型化、単純化及び小スペース化を図りたく、しかも、原料米の種類を問わずに、内在する米澱粉のアルファー化度を自在に変え得て、最適なアルファー化度の米粉を、常に簡単容易に得たいような場合に、利用可能性が極めて高くなる。  The method and apparatus for producing rice flour of the present invention is intended to reduce the size, simplification, and space of the equipment configuration including the wastewater treatment facility, and, regardless of the type of raw rice, When it is possible to freely change the degree of alpha formation and to always obtain rice flour having the optimum degree of alpha formation easily and easily, the availability becomes extremely high.

本発明の米粉の製造方法を示すフロシート図である。  It is a flow sheet figure which shows the manufacturing method of the rice flour of this invention. 本発明の米粉の製造方法を具体化した製造装置のフロシート図である。  It is a flow sheet figure of the manufacturing apparatus which actualized the manufacturing method of the rice flour of this invention. 本発明の米粉の製造装置における洗浄殺菌部のフロシート図である。  It is a flow sheet figure of the washing | cleaning sterilization part in the manufacturing apparatus of the rice flour of this invention. 本発明の米粉の製造装置における洗浄部の組立状態を示す斜視図である。  It is a perspective view which shows the assembly state of the washing | cleaning part in the manufacturing apparatus of the rice flour of this invention. 本発明の米粉の製造装置における蒸し機の一部を切欠した斜視図である。  It is the perspective view which notched some steamers in the rice flour manufacturing apparatus of this invention. 本発明の米粉の製造装置における計量部の一部を断面した側面図である。  It is the side view which carried out the cross section of a part of measurement part in the manufacturing apparatus of the rice flour of this invention. 図1に示す米粉の製造方法における乾燥工程の直前に平板化工程を付加したフロシート図である。  It is the flow sheet figure which added the flattening process just before the drying process in the manufacturing method of the rice flour shown in FIG. 本発明の米粉の製造方法に蒸し米の平板化工程を付加した場合の製造装置のフロシート図である。  It is a flow sheet figure of the manufacturing apparatus at the time of adding the flattening process of steamed rice to the manufacturing method of the rice flour of this invention. 本発明の米粉の製造方法に熟成米の平板化工程を付加した場合の製造装置のフロシート図である。  It is a flow sheet figure of a manufacturing device at the time of adding the flattening process of ripening rice to the manufacturing method of the rice flour of the present invention.

符号の説明Explanation of symbols

1 米粉の製造装置
1A、1Aa 米粉の製造方法
1B 洗浄工程
1C 吸水工程
1D 蒸し工程
1E 乾燥工程
1F 粉化工程
1G 冷却工程
1H 熟成工程
1J 平板化工程
2 米貯留タンク
3 ネット
4 洗浄殺菌部
4A 洗浄部
4B 殺菌部
5 吸水部
6 タンク
6a 底板
6b 側板
6c 孔
7 定量フィーダー
7a モーター
8 蒸し機
9 計量機
10 容器
11 真空冷却包装機
12 熟成ほぐし部
13、13a 乾燥部
14 粉化部
15、39 ロータリーバルブ
16 搬送装置
17、77 バルブ
20 トヨ
21 フタ
22 底板
22a 孔
23 コーン状フード
24 側板
24a、24b、24c 切欠部
25、27 エアー吹出管
26 霧吹出管
28 加圧室
29 減圧室
30 定量供給機
31、81 受入タンク
32 通路
33 振動機
34 ブロワー
35 霧発生用ポンプ
36 噴霧ノズル
37 真空ポンプ
38 米付着物除去タンク
40 米付着物
41 トレー
42 過熱蒸気室
43 蒸気室コンベアー
44 ボイラー
45 常圧過熱水蒸気発生装置
50 湯
51 水槽
52 ネットコンベアー
52a 吸引部
60 排出管
61 直管
62 曲管
63 蒸気室
64 蒸気吹出管
65、65a ホッパー
66 予備ほぐし機
66a パドル
66b ほぐしドラム
67 計量部
68、84 袋
70 第1の工程
71 第2の工程
72 真空発生機
73 第3の工程
74 無菌エアー発生機
75 第4の工程
76 搬送コンベアー
78 上部コンベアー
78a、79a ローラ
79 下部コンベアー
80 袋開封機
82 円筒体
83 掻上機
85 米粉製品
86 品ヤード
90 平板加工機
91 気室コンベアー
92 駆動機
93 無端ベルト
94 押圧ロール
95 受圧ロール
96 過熱蒸気室
R 米
DESCRIPTION OF SYMBOLS 1 Rice flour production apparatus 1A, 1Aa Rice flour production method 1B Washing process 1C Water absorption process 1D Steaming process 1E Drying process 1F Powdering process 1G Cooling process 1H Aging process 1J Flattening process 2 Rice storage tank 3 Net 4 Washing sterilization part 4A Washing Part 4B Sterilization part 5 Water absorption part 6 Tank 6a Bottom plate 6b Side plate 6c Hole 7 Metering feeder 7a Motor 8 Steamer 9 Weighing machine 10 Container 11 Vacuum cooling packaging machine 12 Aging loosening part 13, 13a Drying part 14, Powdering part 15, 39 Rotary Valve 16 Conveying device 17, 77 Valve 20 Toy 21 Lid 22 Bottom plate 22a Hole 23 Cone-shaped hood 24 Side plate 24a, 24b, 24c Notch 25, 27 Air blowing pipe 26 Mist blowing pipe 28 Pressurizing chamber 29 Depressurizing chamber 30 Fixed amount feeder 31, 81 Receiving tank 32 Passage 33 Vibrator 34 Blower 35 Fog generating pump 36 Spray nozzle 37 Vacuum pump 38 Rice deposit removal tank 40 Rice deposit 41 Tray 42 Superheated steam chamber 43 Steam chamber conveyor 44 Boiler 45 Atmospheric pressure superheated steam generator 50 Hot water 51 Water tank 52 Net conveyor 52a Suction part 60 Discharge pipe 61 Straight pipe 62 Curved pipe 63 Steam chamber 64 Steam blow pipe 65, 65a Hopper 66 Preliminary unraveling machine 66a Paddle 66b Unraveling drum 67 Weighing section 68, 84 Bag 70 First step 71 Second step 72 Vacuum generator 73 Third Step 74 Aseptic Air Generator 75 Fourth Step 76 Conveyor 78 Upper Conveyor 78a, 79a Roller 79 Lower Conveyor 80 Bag Opener 82 Cylindrical Body 83 Lifting Machine 85 Rice Flour Product 86 Product Yard 90 Flat Plate Machine 91 Air chamber conveyor 92 93 Endless belt 94 Pressing roll 95 Pressure receiving roll 96 Superheated steam chamber R Rice

Claims (10)

米を洗浄する洗浄工程と、その洗浄後の米を常温の水に20分間〜120分間浸漬してから水切りする吸水工程と、その吸水後の米を飽和水蒸気で予め設定した時間蒸して、少なくとも米澱粉の一部をアルファー化する蒸し工程と、その蒸し米に100℃〜350℃の常圧過熱水蒸気を吹き付けて乾燥する乾燥工程と、その乾燥米を粉砕して粉にする粉化工程と、を含んでなることを特徴とする米粉の製造方法。  A washing step for washing rice, a water absorption step for immersing the washed rice in normal temperature water for 20 to 120 minutes and then draining, and steaming the rice after the water absorption with saturated water vapor for at least a preset time, A steaming step for converting a portion of the rice starch into alpha, a drying step for spraying the steamed rice with normal pressure superheated steam at 100 ° C. to 350 ° C. and drying, and a pulverizing step for crushing the dried rice into powder A method for producing rice flour, comprising: 前記蒸し工程と前記乾燥工程との間に、蒸し米を急速に真空冷却して常温にする冷却工程と、その常温の蒸し米を無菌状態にて24時間〜48時間放置しアルファー化した米澱粉を熟成させる熟成工程と、を付加させた請求項1記載の米粉の製造方法。  Between the steaming step and the drying step, the steamed rice is rapidly vacuum cooled to room temperature, and the steamed rice at room temperature is left in a sterile state for 24 to 48 hours to be alphatized rice starch The method for producing rice flour according to claim 1, further comprising: an aging step of aging the rice. 前記洗浄工程は、ネット上を所定量ずつ流通している米にエアー及び霧を吹き付け洗浄し且つ100℃〜350℃の常圧過熱水蒸気を吹き付けて殺菌してなる請求項1または2記載の米粉の製造方法。  3. The rice flour according to claim 1, wherein the washing step is performed by spraying air and mist on the rice flowing in a predetermined amount on the net and sterilizing by spraying normal pressure superheated steam at 100 ° C. to 350 ° C. 3. Manufacturing method. 前記洗浄工程は、ネット上を所定量ずつ流通している米にエアーを吹き付けると共に吸引して粗洗浄し、その粗洗浄後の米に霧を吹き付けると共に吸引して本洗浄して、その本洗浄後の米にエアーを吹き付けると共に吸引して仕上げ洗浄し、さらにその仕上げ洗浄後の米に100℃〜350℃の常圧過熱水蒸気を吹き付けて殺菌してなる請求項1または2記載の米粉の製造方法。  The cleaning process is performed by blowing air and sucking and coarsely cleaning the rice that has been circulated on the net by a predetermined amount. 3. The production of rice flour according to claim 1 or 2, wherein air is blown into the latter rice and sucked to finish and washed, and then the rice after the finish washing is further sterilized by spraying normal pressure superheated steam at 100 ° C to 350 ° C. Method. 前記蒸し工程と前記乾燥工程との間に、蒸し米を潰して板状にする平板化工程を付加させた請求項1、3または4記載の米粉の製造方法。  The manufacturing method of the rice flour of Claim 1, 3 or 4 which added the flattening process which crushed steamed rice into a plate shape between the said steaming process and the said drying process. 前記熟成工程と前記乾燥工程との間に、熟成米を潰して板状にする平板化工程を付加させた請求項2、3または4記載の米粉の製造方法。  The method for producing rice flour according to claim 2, 3 or 4, wherein a step of flattening the ripened rice into a plate shape is added between the ripening step and the drying step. 米貯留タンクから所定量ずつネット上に受け入れた米にエアー及び霧を吹き付け洗浄し且つ100℃〜350℃の常圧過熱水蒸気を吹き付けて殺菌する洗浄殺菌部と、その洗浄殺菌後の米を30℃〜48℃の湯に20秒間〜10分間さらしてから水切りをする吸水部と、吸水水切り後の米を一定量貯留するタンクの底板及び側板の多数の孔より0.25kg/cm〜1.5kg/cmの飽和蒸気を予め設定した時間吹き込んで蒸し、かつ内部に米を一定量排出する定量フィーダーを有してなる蒸し機と、その蒸し米に100℃〜350℃の常圧過熱水蒸気を吹き付けて乾燥する乾燥部と、その乾燥米を粉砕して粉にする粉化部と、を含んでなることを特徴とする米粉の製造装置。A cleaning and sterilization unit for cleaning by spraying air and mist onto the rice received from the rice storage tank on the net by a predetermined amount and spraying normal pressure superheated steam at 100 ° C. to 350 ° C., and 30 sterilized rice after the cleaning and sterilization 0.25 kg / cm 2 to 1 from a water absorption part that drains water after being exposed to hot water of ℃ to 48 ° C. for 20 seconds to 10 minutes, and a large number of holes in the bottom plate and side plate of the tank that stores a certain amount of rice after draining the water. Steaming with 5 kg / cm 2 of saturated steam blown for a preset time and having a fixed amount feeder that discharges a certain amount of rice inside, and overheating the steamed rice at 100 ° C to 350 ° C at atmospheric pressure An apparatus for producing rice flour, comprising: a drying section that sprays water vapor to dry; and a pulverizing section that pulverizes the dried rice into powder. 前記蒸し機と前記乾燥部との間に、蒸し米を受け入れ予備ほぐしを行うと共にその所定量を計量する計量機と、計量された蒸し米を容器内に入れ閉じて690mmHg以上の真空状態を10秒間〜30秒間保持するようにして常温にしたあと前記容器内から蒸し米を取り出す真空冷却機と、アルファー化した米澱粉を熟成させたあと蒸し米を本ほぐしを行って単粒化した状態とする熟成ほぐし部と、を付加させた請求項5記載の米粉の製造装置。  Between the steamer and the drying unit, steamed rice is received and preliminarily loosened and a predetermined amount is weighed, and the metered steamed rice is put in a container and closed, and a vacuum state of 690 mmHg or more is set to 10 A vacuum cooler for taking steamed rice out of the container after holding at room temperature for 30 to 30 seconds, and aging the pregelatinized rice starch, then unraveling the steamed rice and making it into single grains An apparatus for producing rice flour according to claim 5, further comprising an aging loosening portion to be added. 前記蒸し機と前記乾燥部との間に、無端ベルトとロールとの間に蒸し米を通すことで潰して板状にする平板加工機を付加させた請求項7記載の米粉の製造装置。  The apparatus for producing rice flour according to claim 7, wherein a flat plate processing machine is formed between the steaming machine and the drying unit by crushing steamed rice between an endless belt and a roll to form a plate. 前記熟成ほぐし部と前記乾燥部との間に、無端ベルトとロールとの間に熟成米を通すことで潰して板状にする平板加工機を付加させた請求項8記載の米粉の製造装置。  The apparatus for producing rice flour according to claim 8, wherein a flat plate processing machine is added between the aged loosening unit and the drying unit by crushing aged rice by passing it between an endless belt and a roll.
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KR101033110B1 (en) 2010-03-29 2011-05-11 이주현 Rice milling method
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JP2012223135A (en) * 2011-04-20 2012-11-15 Noriyuki Sugawara Sterile fine rice powder, and method of manufacturing the same
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JP2014207894A (en) * 2013-03-26 2014-11-06 博明 岩本 Method for manufacturing processed fruit, and processed fruit
JP2016112022A (en) * 2013-03-26 2016-06-23 博明 岩本 Method for producing processed fruit
CN107912686A (en) * 2017-11-24 2018-04-17 防城港市绿华源农林科技有限公司 A kind of processing technology thereof of rice edible rice flour
CN113426409A (en) * 2021-05-19 2021-09-24 沈韬 Adsorb active carbon preparation preprocessing device for formaldehyde
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CN114698776A (en) * 2022-05-26 2022-07-05 广东双捷智力素医学科技有限公司 Preparation method and preparation device of edible nutritional rice flour containing ganoderma lucidum spore powder

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